CN203373156U - Lithium iron phosphate battery material complete production system - Google Patents
Lithium iron phosphate battery material complete production system Download PDFInfo
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- CN203373156U CN203373156U CN201320465795.4U CN201320465795U CN203373156U CN 203373156 U CN203373156 U CN 203373156U CN 201320465795 U CN201320465795 U CN 201320465795U CN 203373156 U CN203373156 U CN 203373156U
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Abstract
The utility model discloses a lithium iron phosphate battery material complete production system. The lithium iron phosphate battery material complete production system comprises a head tank 1, a head tank 2, a reaction kettle 3, a spray drying tower 4, an inert atmosphere protective tunnel-based roasting furnace 5, an ultrafine grinder 6, a vibrating screen 7 and a rotary vibration electromagnetic drying machine 8, wherein the head tank 1 and the head tank 2 are jointly connected to the reaction kettle 3 through pipelines; the spray drying tower 4, the inert atmosphere protective tunnel-based roasting furnace 5, the ultrafine grinder 6, the vibrating screen 7 and the rotary vibration electromagnetic drying machine 8 are sequentially connected. The lithium iron phosphate battery material complete production system has the advantages that the equipment is simple and easy to obtain, the productivity cooperation is balanced, a production technology matched with the equipment is simple, raw materials are easily available and cheap, produced products have excellent properties, and the lithium iron phosphate battery material complete production system belongs to a clean production system.
Description
Technical field
The utility model relates to a kind of complete production unit and composition system thereof of ferric phosphate lithium cell material.
Background technology
The olivine-type iron lithium phosphate, due to the anode material for lithium-ion batteries that cycle performance is excellent, safety performance is good, cheap, the starting material wide material sources are considered to have most DEVELOPMENT PROSPECT and potentiality, is one of lithium ion battery material that research is the most popular at present, industrialization is maximum.
The starting material selection of producing iron lithium phosphate is more extensive, and the production equipment system matched with it also has larger difference because of the selection of raw material.Adopting Ferrox, Quilonum Retard and primary ammonium phosphate is raw material or to adopt tertiary iron phosphate and Quilonum Retard be raw material, is generally high temperature solid-state method, uses liquid phase ball milling, vacuum drying process, then high-temperature roasting; Adopting ferrous sulfate, lithium hydroxide, phosphoric acid or ammonium phosphate is raw material, is generally liquid phase method or hydrothermal method, uses the synthetic presoma of hydrothermal reaction kettle of liquid phase reaction still or High Temperature High Pressure, low-temperature heat treatment then, then carry out the high-temperature roasting of short period of time.
But above-mentioned adopted raw material and production technique, whole manufacturing process is longer, and cost of raw and processed materials and production cost are all higher, are unfavorable for reducing production cost and the extensive industrialization of LiFePO 4 material.
Summary of the invention
The purpose of this utility model is to overcome the deficiency of above-mentioned prior art and complete production system that the ferric phosphate lithium cell material that a kind of cost is low, equipment is simple is provided.
The purpose of this utility model can reach by following measure: a kind of complete production system of ferric phosphate lithium cell material; it is characterized in that comprising header tank 1, header tank 2 jointly by pipeline access reactor 3, reactor 3 connects spray-drying tower 4 by pipeline, and the inert atmosphere protection tunnel like stoving oven 5, ultrafine crusher 6, the vibratory screening apparatus 7 that connect successively and revolve the electromagnetic drying machine 8 that shakes and form.
In order further to realize the purpose of this utility model, the bottom of described header tank 1 and header tank 2 is higher than reactor 3 upper surfaces.
It is raw material that this complete production system adopts phosphoric acid solution, lithium hydroxide solution, ferric oxide, doped element, organic carbon source; through mixing in reactor; form the slurry containing ferric oxide, phosphate radical, lithium ion and dopant ion, organic carbon source; in spraying drying, rapid drying forms presoma; in the inert atmosphere protection high-temperature roasting; through pulverizing, sieving, dewater, form the ferric phosphate lithium cell material again.
The utility model can produce following positively effect compared with the prior art: native system equipment is simple and easy to get, and production capacity coordinates balanced, simple with the production technique of coordinative composition of equipments, the starting material cheapness that is easy to get, and the excellent product performance of production, belong to clean-production system.
The accompanying drawing explanation
Fig. 1 is the equipment connecting relation schematic diagram of the utility model production system.
Wherein, 1, header tank 1; 2, header tank 2; 3, reactor; 4, spray-drying tower; 5, the tunnel like stoving oven of inert atmosphere protection; 6, ultrafine crusher; 7, vibratory screening apparatus; 8, revolve the electromagnetic drying machine that shakes.
Embodiment
A kind of complete production system (as shown in Fig. 1) of ferric phosphate lithium cell material, comprise header tank 1, header tank 2 jointly by pipeline access reactor 3, reactor 3 connects spray-drying tower 4 by pipeline, and the tunnel like stoving oven 5, ultrafine crusher 6, the vibratory screening apparatus 7 that connect successively and revolve the electromagnetic drying machine 8 that shakes and form.Wherein the bottom of header tank 1 and header tank 2 is higher than reactor 3 upper surfaces.
Concrete operations are as follows: certain density phosphoric acid solution is stored in header tank 1, certain density lithium hydroxide solution is stored in header tank 2, open two pipeline valves that header tank is connected with reactor 3, open the stirring rake of reactor 3 simultaneously, phosphoric acid solution and lithium hydroxide solution flow in reactor 3 and fully react lentamente, then add ferric oxide, doped element, organic carbon sources etc. are former to be expected in reactor 3, squeeze into rapid drying in spray-drying tower after mixing, form spherical presoma, high-temperature roasting through the tunnel like stoving oven 800 degree left and right in the nitrogen atmosphere protection, form the black iron phosphate powder, then in ultrafine crusher, crushing and classification obtains the powdered material of 2～5 microns, after 325 purpose ultrasonic vibration sieve screenings, in revolving the electromagnetic drying machine that shakes rapid drying remove crushing process in the moisture of material surface absorption, obtain even particle size distribution, inclusion-free, water-content is lower than the ferric phosphate lithium cell material of 800ppm.
Claims (2)
1. the complete production system of a ferric phosphate lithium cell material; it is characterized in that comprising header tank (1), header tank (2) jointly by pipeline access reactor (3), reactor (3) connects spray-drying tower (4) by pipeline, and tunnel like stoving oven (5), ultrafine crusher (6), the vibratory screening apparatus (7) of the inert atmosphere protection connected successively and revolve electromagnetic drying machine (8) formation of shaking.
2. according to the complete production system of a kind of ferric phosphate lithium cell material claimed in claim 1, it is characterized in that the bottom of described header tank (1) and header tank (2) is higher than reactor (3) upper surface.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320465795.4U CN203373156U (en) | 2013-08-01 | 2013-08-01 | Lithium iron phosphate battery material complete production system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320465795.4U CN203373156U (en) | 2013-08-01 | 2013-08-01 | Lithium iron phosphate battery material complete production system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203373156U true CN203373156U (en) | 2014-01-01 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201320465795.4U Expired - Lifetime CN203373156U (en) | 2013-08-01 | 2013-08-01 | Lithium iron phosphate battery material complete production system |
Country Status (1)
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104599808A (en) * | 2014-12-29 | 2015-05-06 | 东莞市凯金新能源科技有限公司 | Rotary demagnetizer and lithium battery negative electrode material powder processing device |
| CN107062823A (en) * | 2017-04-17 | 2017-08-18 | 厦门高容新能源科技有限公司 | A kind of material surface cladding and high-temperature process combined unit |
| CN108408710A (en) * | 2018-04-25 | 2018-08-17 | 深圳市寒暑科技新能源有限公司 | A kind of energy conservation and environmental protection prepares the device and preparation method of LiFePO4 |
-
2013
- 2013-08-01 CN CN201320465795.4U patent/CN203373156U/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104599808A (en) * | 2014-12-29 | 2015-05-06 | 东莞市凯金新能源科技有限公司 | Rotary demagnetizer and lithium battery negative electrode material powder processing device |
| CN107062823A (en) * | 2017-04-17 | 2017-08-18 | 厦门高容新能源科技有限公司 | A kind of material surface cladding and high-temperature process combined unit |
| CN108408710A (en) * | 2018-04-25 | 2018-08-17 | 深圳市寒暑科技新能源有限公司 | A kind of energy conservation and environmental protection prepares the device and preparation method of LiFePO4 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee |
Owner name: YANTAI ZHUONENG BATTERY MATERIALS CO., LTD. Free format text: FORMER NAME: YANTAI ZHUONENG BATTERY MATERIAL CO., LTD. |
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| CP01 | Change in the name or title of a patent holder |
Address after: 264002 No. 45, Chemical Road, Zhifu District, Shandong, Yantai Patentee after: YANTAI ZHUONENG BATTERY MATERIAL Co.,Ltd. Address before: 264002 No. 45, Chemical Road, Zhifu District, Shandong, Yantai Patentee before: YANTAI ZHUONENG BATTERY MATERIAL Co.,Ltd. |
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| TR01 | Transfer of patent right |
Effective date of registration: 20200413 Address after: 264003 12 / F, Tower B, Guanhai building, Guanhai Road, Laishan District, Yantai City, Shandong Province Patentee after: Yantai state owned Assets Management Co.,Ltd. Address before: 264002 No. 45, Chemical Road, Zhifu District, Shandong, Yantai Patentee before: YANTAI ZHUONENG BATTERY MATERIAL Co.,Ltd. |
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| TR01 | Transfer of patent right | ||
| CX01 | Expiry of patent term |
Granted publication date: 20140101 |
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| CX01 | Expiry of patent term |